Organometallic aluminum fumarate backbone material

ABSTRACT

Porous metal organic frameworks formed by Al III  ions to which fumarate ions are coordinated to produce a framework structure; shaped bodies comprising such porous metal organic frameworks, and also the preparation and use thereof for the uptake of a substance for the purposes of its storage, controlled release, separation, chemical reaction or as support.

The present invention relates to a porous metal organic framework,shaped bodies comprising this, a process for preparing the framework andits use.

Porous metal organic frameworks are known from the prior art. They aredistinguished, in particular, by their porosity and can frequently beemployed in applications comparable to those which are known forinorganic zeolites.

Metal organic frameworks usually comprise an at least bidentate organiccompound coordinated to a metal ion to form the skeleton of the metalorganic framework.

An appropriate choice of metal and/or organic compound makes it possibleto optimize the framework for the desired field of application. Forexample, the choice of the organic compound can exert an influence onthe pore distribution. In addition, the metal can make a contribution inadsorption processes.

There is thus a continual need to provide specific metal organicframeworks which, in particular, have extraordinary propertiesattributable to the choice of the metal and of the organic compound.

One interesting metal is aluminum since comparatively robust metalorganic frameworks can be obtained as a result of strong coordinatebonds. In addition, the aluminum ion is, due to its octahedralcoordination, in principle capable of building up three-dimensionalframework compounds. Furthermore, the salts of aluminum used as startingmaterials are readily available and inexpensive.

It is therefore an object of the present invention to provide frameworkswhich are based on aluminum and have particular properties, especiallyin respect of the storage and separation of chemical substances such asgases.

The object is achieved by a porous metal organic framework formed byAl^(III) ions to which fumarate ions are coordinated to produce aframework structure.

It has been found that the porous metal organic framework formed byaluminum ions and fumarate ions (trans-1,2-ethylenedicarboxylate)surprisingly has a one-dimensional channel structure which additionallydisplays a surprising high specific surface area, so that the metalorganic framework of the present invention can be particularly usefulfor the storage and separation of chemical substances, in particulargases.

The porous metal organic framework of the invention thus has aone-dimensional channel structure which crystallizes in the orthorhombicsystem.

The structure of the porous metal organic framework of the invention canbe recognized, in particular, by the X-ray diffraction pattern (XRD)having a basic reflection in the range 8°<2Θ<12°.

FIG. 1 shows the X-ray diffraction pattern of the porous metal organicframework of the invention. Here, the intensity I (Lin(counts)) is shownas a function of the 2 theta scale (2Θ).

Here, the diffraction pattern can be recorded as follows: the sample isinstalled as a powder in the sample container of a commerciallyavailable instrument (Siemens D-5000 diffractometer or BrukerD8-Advance). Cu-Kα radiation with variable primary and secondaryapertures and secondary monochromator is used as radiation source. Thesignal is detected by means of a scintillation detector (Siemens) orSolex semiconductor detector (Bruker). The measurement range for 2Θ istypically chosen as from 2° to 70°. The angle step is 0.02°, and themeasurement time per angle step is typically from 2 to 4 seconds. In theevaluation, reflections are distinguished by a signal strength which isat least 3 times as high as the background noise. An area analysis canbe carried out manually by drawing a baseline under the individualreflections. As an alternative, programs such as “Topas-Profile” fromBruker can be used, in which case the background smoothing thenpreferably occurs automatically via a 1st order polynomial in thesoftware.

The framework of the invention has a one-dimensional channel structurein which linear chains of Al^(III) ions and OH groups are bridged by theorganic fumarate to give a three-dimensional, orthorhombic structure.

The metal organic framework of the invention can be present in powderform or as agglomerate.

The porous metal organic framework of the invention can be used as suchin powder form or is converted into a shaped body.

Accordingly, a further aspect of the present invention is the porousmetal organic framework of the invention in powder form.

A further aspect of the present invention is accordingly a shaped bodycomprising the porous metal organic framework of the invention.

The production of shaped bodies comprising metal organic frameworks isdescribed, for example, in WO-A 03/102000.

Here, preferred processes for producing shaped bodies are extrusion andtableting. In the production of the shaped bodies, the framework can bepresent in a mixture with further materials, for example binders,lubricants or other additives, which are added during production. It islikewise conceivable for the framework to comprise further constituents,for example absorbents such as activated carbon or the like.

The possible geometries of the shaped bodies are essentially not subjectto any restrictions. Examples which may be mentioned are, inter alia,pellets such as disk-shaped pellets, pills, spheres, granules,extrudates such as rods, honeycombs, grids or hollow bodies.

To produce these shaped bodies, it is in principle possible to employall suitable methods. In particular, the following processes arepreferred:

-   -   Kneading/pan milling of the framework either alone or together        with at least one binder and/or at least one pasting agent        and/or at least one template compound to give a mixture; shaping        of the resulting mixture by means of at least one suitable        method such as extrusion; optionally washing and/or drying        and/or calcination of the extrudate; optionally finishing        treatment.    -   Tableting together with at least one binder and/or another        auxiliary.    -   Application of the framework to at least one optionally porous        support material. The material obtained can then be processed        further by the above-described method to give a shaped body.    -   Application of the framework to at least one optionally porous        substrate.

Kneading/pan milling and shaping can be carried out by any suitablemethod, for example as described in Ullmanns Enzyklopädie derTechnischen Chemie, 4th edition, volume 2, p. 313 ff, (1972).

For example, the kneading/pan milling and/or shaping can be carried outby means of a piston press, roller press in the presence or absence ofat least one binder, compounding, pelletization, tableting, extrusion,coextrusion, foaming, spinning, coating, granulation, preferably spraygranulation, spraying, spray drying or a combination of two or more ofthese methods.

Very particular preference is given to producing pellets and/or tablets.

The kneading and/or shaping can be carried out at elevated temperatures,for example in the range from room temperature to 300° C., and/or undersuperatmospheric pressure, for example in the range from atmosphericpressure to a few hundred bar, and/or in a protective gas atmosphere,for example in the presence of at least one noble gas, nitrogen or amixture of two or more thereof.

The kneading and/or shaping is, in a further embodiment, carried outwith addition of at least one binder, with the binder used basicallybeing able to be any chemical compound which ensures the viscositydesired for the kneading and/or shaping of the composition to be kneadedand/or shaped. Accordingly, binders can, for the purposes of the presentinvention, be either viscosity-increasing or viscosity-reducingcompounds.

Preferred binders are, for example, inter alia, aluminum oxide orbinders comprising aluminum oxide, as are described, for example, in WO94/29408, silicon dioxide as described, for example, in EP 0 592 050 A1,mixtures of silicon dioxide and aluminum oxide, as are described, forexample, in WO 94/13584, clay minerals as described, for example, in JP03-037156 A, for example montmorillonite, kaolin, bentonite, halloysite,dickite, nacrite and anauxite, alkoxysilanes as are described, forexample, in EP 0 102 544 B1, for example tetraalkoxysilanes such astetramethoxysilane, tetraethoxysilane, tetrapropoxysilane,tetrabutoxysilane, or, for example, trialkoxysilanes such astrimethoxysilane, triethoxysilane, tripropoxysilane, tributoxysilane,alkoxytitanates, for example tetralkoxytitanates such astetramethoxytitanate, tetraethoxytitanate, tetrapropoxytitanate,tetrabutoxytitanate, or, for example, trialkoxytitanates such astrimethoxytitanate, triethoxytitanate, tripropoxytitanate,tributoxytitanate, alkoxyzirconates, for example tetralkoxyzirconatessuch as tetramethoxyzirconate, tetraethoxyzirconate,tetrapropoxyzirconate, tetrabutoxyzirconate, or, for example,trialkoxyzirconates such as trimethoxyzirconate, triethoxyzirconate,tripropoxyzirconate, tributoxyzirconate, silica sols, amphiphilicsubstances and/or graphites.

As viscosity-increasing compound, it is, for example, also possible touse, if appropriate in addition to the abovementioned compounds, anorganic compound and/or a hydrophilic polymer such as cellulose or acellulose derivative such as methylcellulose and/or a polyacrylateand/or a polymethacrylate and/or a polyvinyl alcohol and/or apolyvinylpyrrolidone and/or a polyisobutene and/or a polytetrahydrofuranand/or a polyethylene oxide.

As pasting agent, it is possible to use, inter alia, preferably water orat least one alcohol such as a monoalcohol having from 1 to 4 carbonatoms, for example methanol, ethanol, n-propanol, isopropanol,1-butanol, 2-butanol, 2-methyl-1-propanol or 2-methyl-2-propanol or amixture of water and at least one of the alcohols mentioned or apolyhydric alcohol such as a glycol, preferably a water-misciblepolyhydric alcohol, either alone or as a mixture with water and/or atleast one of the monohydric alcohols mentioned.

Further additives which can be used for kneading and/or shaping are,inter alia, amines or amine derivatives such as tetraalkylammoniumcompounds or amino alcohols and carbonate-comprising compounds such ascalcium carbonate. Such further additives are described, for instance,in EP 0 389 041 A1, EP 0 200 260 A1 or WO 95/19222.

The order of the additives such as template compound, binder, pastingagent, viscosity-increasing substance during shaping and kneading is inprinciple not critical.

In a further preferred embodiment, the shaped body obtained by kneadingand/or shaping is subjected to at least one drying step which isgenerally carried out at a temperature in the range from 25 to 500° C.,preferably in the range from 50 to 500° C. and particularly preferablyin the range from 100 to 350° C. It is likewise possible to carry outdrying under reduced pressure or under a protective gas atmosphere or byspray drying.

In a particularly preferred embodiment, at least one of the compoundsadded as additives is at least partly removed from the shaped bodyduring this drying process.

The metal organic framework of the invention comprises pores, inparticular micropores and/or mesopores. Micropores are defined as poreshaving a diameter of 2 nm or less and mesopores are defined by adiameter in the range from 2 to 50 nm (Pure & Appl. Chem. 57 (1985)603-619). The presence of micropores and/or mesopores can be checked bymeans of sorption measurements, with these measurements determining theuptake capacity of the metal organic frameworks for nitrogen at 77kelvin (Langmuir method) in accordance with DIN 66131 and/or DIN 66134.

The pores are preferably present in the form of one-dimensional channelshaving a diameter of from 5 to 15 angström, particularly preferably from7 to 12 Å.

The specific surface area, calculated according to the Langmuir model(DIN 66131, 66134), of the metal organic framework of the invention inpowder form is preferably at least 1000 m²/g, more preferably at least1200 m²/g, more preferably at least 1400 m²/g, even more preferably atleast 1600 m²/g, even more preferably at least 1800 m²/g andparticularly preferably at least 1950 m²/g.

Shaped bodies comprising the metal organic framework of the inventioncan have a lower specific surface area, but preferably at least 500m²/g, more preferably at least 600 m²/g, even more preferably at least700 m²/g, in particular at least 800 m²/g.

The present invention further provides a process for preparing a porousmetal organic framework according to the invention, which comprises thestep

-   -   reaction of a reaction mixture comprising at least one aluminum        compound and fumaric acid or a salt thereof in the presence of        an organic solvent at a predetermined temperature and a        predetermined pressure.

The organic component of the porous metal organic framework of theinvention is fumaric acid which can be reacted with an aluminumcompound. It is likewise possible to use derivatives of fumaric acid.Thus, for example, it is conceivable to use fumaric acid in the form ofits salt. The salt, in which fumaric acid is present as completely orpartially deprotonated anion, can have any suitable cation.

Such cations can be, for example, monovalent or divalent, preferablymonovalent, metal ions. Examples are, in particular, sodium andpotassium salts. It is likewise possible to use cations of ammoniumcompounds. Here, particular mention may be made of ammonium itself andalso alkylammonium cations.

The aluminum compound can be produced by anodic oxidation of metallicaluminum. In such a case the porous metal organic framework of theinvention is prepared by an at least partly electrochemical route.Processes for the electrochemical preparation of porous metal organicframeworks are described in WO-A 2005/049892. The aluminum compound forthe porous metal organic framework of the invention can also be producedby this route.

In the electrochemical preparation of the porous metal organic frameworkof the invention, preference is given to cathodic redeposition of thealuminum ion being at least partly prevented by means of at least one ofthe following measures:

-   -   (i) use of an electrolyte which promotes cathodic formation of        hydrogen;    -   (ii) addition of at least one compound which leads to cathodic        depolarization;    -   (iii) use of a cathode having a suitable hydrogen overvoltage.

The process can be carried out in an undivided electrolysis cell.Especially useful cells are gap cells or stacked plate cells. These canbe connected in a bipolar fashion. Suitable reaction media are, forexample, methanol, ethanol, dimethylformamide, diethylformamide or amixture of two or more of these solvents.

An electrolyte salt or a plurality of electrolyte salts can also bepresent in the reaction mixture. Here, the electrolyte salt can have aquaternary ammonium ion as cation component and an alkoxysulfate ion asanion component. The total solids content should be greater than orequal to 0.5% by weight.

The reaction in the process of the invention for preparing the metalorganic framework of the invention can also be carried out by aclassical route. Here, the aluminum compound is typically an aluminumsalt.

The aluminum salt can be present in the form of an alkoxide, acetonate,halide, sulfite, as a salt of an organic or inorganic, oxygen-comprisingacid or a mixture thereof.

An alkoxide is, for example, a methoxide, ethoxide, n-propoxide,i-propoxide, n-butoxide, i-butoxide, t-butoxide or phenoxide.

An acetonate is, for example, acetylacetonate.

A halide is, for example, chloride, bromide or iodide.

An organic, oxygen-comprising acid is, for example, formic acid, aceticacid, propionic acid or another alkylmonocarboxylic acid.

An inorganic, oxygen-comprising acid is, for example, sulfuric acid,sulfurous acid, phosphoric acid or nitric acid.

More preferred aluminum compounds are inorganic aluminum salts such asaluminum chloride, aluminum bromide, aluminum hydrogensulfate, aluminumdihydrogen phosphate, aluminum monohydrogen phosphate, aluminumphosphate, aluminum nitrate.

The aluminum compound can, if appropriate, comprise water of hydration,which is preferred. Particularly preferred aluminum compounds are thehydrates of the chloride, nitrate and sulfate.

The reaction in the process of the invention for preparing the porousmetal organic framework of the invention is carried out at least in thepresence of an organic solvent. Here, solvothermal conditions can beused.

For the purposes of the present invention, the term “thermal” refers toa preparative process in which the reaction to form the porous metalorganic framework of the invention is carried out in a pressure vesselwhich is closed during the reaction and to which elevated temperature isapplied so that a pressure builds up within the reaction medium in thepressure vessel as a result of the vapor pressure of the solventpresent.

The reaction preferably does not occur in a water-comprising medium andthus not under solvothermal conditions.

Accordingly, the reaction in the process of the invention preferablyoccurs in the presence of a nonaqueous solvent.

The reaction is preferably carried out at a pressure of from 1 bar to 16bar (absolute), preferably from 1 to 3 bar (absolute). However, thepressure is more preferably not more than 1230 mbar (absolute). Thereaction particularly preferably takes place at atmospheric pressure.However, slight superatmospheric or subatmospheric pressures can occurdue to the apparatus. For the purposes of the present invention, theterm “atmospheric pressure” therefore refers to the pressure range givenby the actual atmospheric pressure ±150 mbar.

The reaction preferably takes place in a temperature range from 100° C.to 200° C. The temperature is preferably in the range from 110° C. to170° C. The temperature is more preferably in the range from 120° C. to150° C.

The reaction mixture can further comprise a base. This serves, inparticular, to ensure that when the carboxylic acid is used as at leastbidentate organic compound, this is readily soluble. When an organicsolvent is used, it is frequently not necessary to add such a base.Nevertheless, the solvent for the process of the invention can beselected so that it itself is basic, but this is not absolutelynecessary for carrying out the process of the invention.

It is likewise possible to use a base. However, preference is given tono additional base being used.

Furthermore, it is advantageous for the reaction to be able to takeplace with stirring, which is also advantageous in a scale-up.

The (nonaqueous) organic solvent is preferably a C₁₋₆-alkanol, dimethylsulfoxide (DMSO), N,N-dimethylformamide (DMF), N,N-diethylformamide(DEF), N,N-dimethylacetamide (DMAc), acetonitrile, toluene, dioxane,benzene, chlorobenzene, methyl ethyl ketone (MEK), pyridine,tetrahydrofuran (THF), ethyl acetate, optionally halogenatedC₁₋₂₀₀-alkane, sulfolane, glycol, N-methylpyrrolidone (NMP),gamma-butyrolactone, alicyclic alcohols such as cyclohexanol, ketonessuch as acetone or acetylacetone, cyclic ketones such as cyclohexanone,sulfolene or mixtures thereof.

A C₁₋₆-alkanol is an alcohol having from 1 to 6 carbon atoms. Examplesare methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol,t-butanol, pentanol, hexanol and also mixtures thereof.

An optionally halogenated C₁₋₂₀₀-alkane is an alkane which has from 1 to200 carbon atoms and in which one or more up to all hydrogen atoms canbe replaced by halogen, preferably chlorine or fluorine, in particularchlorine. Examples are chloroform, dichloromethane, tetrachloromethane,dichloroethane, hexane, heptane, octane and mixtures thereof.

Preferred solvents are DMF, DEF, DMAc and NMP. Particular preference isgiven to DMF.

The term “nonaqueous” preferably refers to a solvent which does notexceed a maximum water content of 10% by weight, more preferably 5% byweight, even more preferably 1% by weight, more preferably 0.1% byweight, particularly preferably 0.01% by weight, based on the totalweight of the solvent.

The maximum water content during the reaction is preferably 10% byweight, more preferably 5% by weight and even more preferably 1% byweight.

The term “solvent” encompasses pure solvents and mixtures of varioussolvents.

Furthermore, the process step of reaction of the at least one metalcompound with the at least one at least bidentate organic compound ispreferably followed by a calcination step. The temperature set here istypically above 250° C., preferably from 300 to 400° C.

The at least bidentate organic compound present in the pores can beremoved by means of the calcination step.

In addition or as an alternative thereto, the removal of the at leastbidentate organic compound (ligand) from the pores of the porous metalorganic framework can be effected by treatment of the framework formedwith a nonaqueous solvent. Here, the ligand is removed in a type of“extraction process” and may be replaced by a solvent molecule in theframework.

The treatment is preferably carried out for at least 30 minutes and cantypically be carried out for up to 7 days. This can occur at roomtemperature or elevated temperature. It preferably takes place atelevated temperature, for example at at least 40° C., preferably 60° C.The extraction more preferably takes place at the boiling point of thesolvent used (under reflux).

The treatment can be carried out in a simple vessel by slurrying andstirring of the framework. It is also possible to use extractionapparatuses such as Soxhlet apparatuses, in particular industrialextraction apparatuses.

As suitable solvents, it is possible to use those mentioned above, i.e.,for example, C₁₋₆-alkanol, dimethyl sulfoxide (DMSO),N,N-dimethylformamide (DMF), N,N-diethylformamide (DEF),N,N-dimethylacetamide (DMAc), acetonitrile, toluene, dioxane, benzene,chlorobenzene, methyl ethyl ketone (MEK), pyridine, tetrahydrofuran(THF), ethyl acetate, optionally halogenated C₁₋₂₀₀-alkane, sulfolane,glycol, N-methylpyrrolidone (NMP), gamma-butyrolactone, alicyclicalcohols such as cyclohexanol, ketones such as acetone or acetylacetone,cyclic ketones such as cyclohexanone or mixtures thereof.

Preference is given to methanol, ethanol, propanol, acetone, MEK andmixtures thereof.

A very particularly preferred extraction solvent is methanol.

The solvent used for the extraction can be identical to or differentfrom that for the reaction of the at least one metal compound with theat least one at least bidentate organic compound. It is not absolutelynecessary in the “extraction” but preferred that the solvent iswater-free.

It is preferred that the molar ratio of aluminum compound to fumaricacid or one of its salts in the process of the invention is in the rangefrom 0.3:1 to 1.7:1. The ratio is more preferably in the range from0.7:1 to 1.2:1.

The present invention further provides for the use of a porous metalorganic framework according to the invention for the uptake of at leastone substance for the purposes of its storage, separation, controlledrelease, chemical reaction or as support.

The at least one substance is preferably a gas or a gas mixture. Liquidsare also possible.

Processes for storage by means of metal organic frameworks in generalare described in WO-A 2005/003622, WO-A 2003/064030, WO-A 2005/049484,WO-A 2006/089908 and DE-A 10 2005 012 087. The processes described therecan also be used for the metal organic framework of the invention.Preferred gases for storage are methane or hydrogen.

Processes for separation or purification by means of metal organicframeworks in general are described in EP-A 1 674 555, DE-A 10 2005000938 and the German patent application number DE-A 10 2005 022 844.The processes described there can also be used for the metal organicframework of the invention. A preferred gas to be separated off iscarbon dioxide, in particular from a gas mixture which further comprisescarbon monoxide.

If the porous metal organic framework of the invention is used forstorage, this preferably takes place in a temperature range from −200°C. to +80° C. A greater preference is given to a temperature range from−40° C. to +80° C. A preferred pressure range is from 20 bar to 1000 bar(absolute), in particular from 100 bar to 400 bar.

For the purposes of the present invention, the terms “gas” and “liquid”are used in the interests of simplicity, but gas mixtures and liquidmixtures or liquid solutions are likewise encompassed by the term “gas”or “liquid”, respectively.

Preferred gases are hydrogen, natural gas, town gas, hydrocarbons, inparticular methane, ethane, ethene, acetylene, propane, n-butane andi-butane, carbon monoxide, carbon dioxide, nitrogen oxides, oxygen,sulfur oxides, halogens, halogenated hydrocarbons, NF₃, SF₆, ammonia,boranes, phosphanes, hydrogen sulfide, amines, formaldehyde, noblegases, in particular helium, neon, argon, krypton and xenon.

The gas is particularly preferably carbon dioxide which is separated offfrom a gas mixture comprising carbon dioxide. The gas mixture preferablycomprises carbon dioxide together with at least H₂, CH₄ or carbonmonoxide. In particular, the gas mixture comprises carbon dioxidetogether with carbon monoxide. Very particular preference is given tomixtures which comprise at least 10% by volume and not more than 45% byvolume of carbon dioxide and at least 30% by volume and not more than90% by volume of carbon monoxide.

A preferred embodiment is pressure swing adsorption using a plurality ofparallel adsorber reactors, with the adsorbent bed consisting entirelyor partly of the material of the invention. In the case of CO₂/COseparation, the adsorption phase preferably takes place at a CO₂ partialpressure of from 0.6 to 3 bar and a temperature of at least 20° C. butnot more than 70° C. To desorb the adsorbed carbon dioxide, the totalpressure in the adsorber reactor concerned is usually reduced to valuesin the range from 100 mbar to 1 bar.

Preference is also given to the use of the framework of the inventionfor storage of a gas at a minimum pressure of 100 bar (absolute). Theminimum pressure is more preferably 200 bar (absolute), in particular300 bar (absolute). Here, the gas is particularly preferably hydrogen ormethane.

However, the at least one substance can also be a liquid. Examples ofsuch a liquid are disinfectants, inorganic or organic solvents, fuels,in particular gasoline or diesel, hydraulic fluids, radiator fluids,brake fluids or an oil, in particular machine oil. Furthermore, theliquid can be a halogenated aliphatic or aromatic, cyclic or acyclichydrocarbon or a mixture thereof. In particular, the liquid can beacetone, acetonitrile, aniline, anisole, benzene, benzonitrile,bromobenzene, butanol, tert-butanol, quinoline, chlorobenzene,chloroform, cyclohexane, diethylene glycol, diethyl ether,dimethylacetamide, dimethylformamide, dimethyl sulfoxide, dioxane,glacial acetic acid, acetic anhydride, ethyl acetate, ethanol, ethylenecarbonate, ethylene dichloride, ethylene glycol, ethylene glycoldimethyl ether, formamide, hexane, isopropanol, methanol,methoxypropanol, 3-methyl-1-butanol, methylene chloride, methyl ethylketone, N-methylformamide, N-methylpyrrolidone, nitrobenzene,nitromethane, piperidine, propanol, propylene carbonate, pyridine,carbon disulfide, sulfolane, tetrachloroethene, carbon tetrachloride,tetrahydrofuran, toluene, 1,1,1-trichloroethane, trichloroethylene,triethylamine, triethylene glycol, triglyme, water or a mixture thereof.

The at least one substance can also be an odorous substance.

The odorous substance is preferably a volatile organic or inorganiccompound which comprises at least one of the elements nitrogen,phosphorus, oxygen, sulfur, fluorine, chlorine, bromine or iodine or anunsaturated or aromatic hydrocarbon or a saturated or unsaturatedaldehyde or a ketone. More preferred elements are nitrogen, oxygen,phosphorus, sulfur, chlorine, bromine; and particular preference isgiven to nitrogen, oxygen, phosphorus and sulfur.

In particular, the odorous substance is ammonia, hydrogen sulfide,sulfur oxides, nitrogen oxides, ozone, cyclic or acyclic amines, thiols,thioethers and also aldehydes, ketones, esters, ethers, acids oralcohols, Particular preference is given to ammonia, hydrogen sulfide,organic acids (preferably acetic acid, propionic acid, butyric acid,isobutyric acid, valeric acid, isovaleric acid, caproic acid, heptanoicacid, lauric acid, pelargonic acid) and cyclic or acyclic hydrocarbonswhich comprise nitrogen or sulfur and also saturated or unsaturatedaldehydes such as hexanal, heptanal, octanal, nonanal, decanal, octenalor nonenal and in particular volatile aldehydes such as butyraldehyde,propionaldehyde, acetaldehyde and formaldehyde and also fuels such asgasoline, diesel (constituents).

The odorous substances can also be fragrances which are used, forexample, for producing perfumes. Examples of fragrances or oils whichrelease such fragrances are: essential oils, basil oil, geranium oil,mint oil, cananga oil, cardamom oil, lavender oil, peppermint oil,nutmeg oil, Camilla oil, eucalyptus oil, rosemary oil, lemon oil, limeoil, orange oil, bergamot oil, muscatel sage oil, coriander oil, cypressoil, 1,1-dimethoxy-2-phenylethane, 2,4-dimethyl-4-phenyltetrahydrofuran,dimethyltetrahydrobenzaldehyde, 2,6-dimethyl-7-octen-2-ol,1,2-diethoxy-3,7-dimethyl-2,6-octadiene, phenylacetaldehyde, rose oxide,ethyl-2-methylpentanoate,1-(2,6,6-trimethyl-1,3-cyclohexadien-1-yl)-2-buten-1-one, ethylvanillin, 2,6-dimethyl-2-octenol, 3,7-dimethyl-2-octenol,tert-butylcyclohexyl acetate, anisyl acetate, allylcyclohexyloxyacetate, ethyllinalool, eugenol, coumarin, ethylacetoacetate, 4-phenyl-2,4,6-trimethyl-1,3-dioxane,4-methylene-3,5,6,6-tetramethyl-2-heptanone, ethyl tetrahydrosafranate,geranyl nitrile, cis-3-hexen-1-ol, cis-3-hexenyl acetate, cis-3-hexenylmethyl carbonate, 2,6-dimethyl-5-hepten-1-al,4-(tricyclo[5.2.1.0]decylidene)-8-butanal,5-(2,2,3-trimethyl-3-cyclopentenyl)-3-methylpentan-2-ol,p-tert-butyl-alpha-methylhydrocinnamaidehyde,ethyl[5.2.1.0]tricyclodecanecarboxylate, geraniol, citronellol, citral,linalool, linalyl acetate, ionone, phenylethanol and mixtures thereof.

For the purposes of the present invention, a volatile odorous substancepreferably has a boiling point or boiling range below 300° C. Theodorous substance is more preferably a readily volatile compound ormixture. The odorous substance particularly preferably has a boilingpoint or boiling range below 250° C., more preferably below 230° C.,particularly preferably below 200° C.

Preference is likewise given to odorous substances which have a highvolatility. The vapor pressure can be employed as a measure of thevolatility. For the purposes of the present invention, a volatileodorous substance preferably has a vapor pressure of more than 0.001 kPa(20° C.). The odorous substance is more preferably a readily volatilecompound or mixture. The odorous substance particularly preferably has avapor pressure of more than 0.01 kPa (20° C.), more preferably a vaporpressure of more than 0.05 kPa (20° C.). Particular preference is givento the odorous substances having a vapor pressure of more than 0.1 kPa(20° C.).

An example in which a chemical reaction can take place in the presenceof the metal organic framework of the invention is the alkoxylation ofmonools or polyols. The procedure for carrying out such alkoxylations isdescribed in WO-A 03/035717 and WO-A 2005/03069. The porous metalorganic framework of the invention can likewise be used for epoxidationand for preparing polyalkylene carbonates and hydrogen peroxide. Suchreactions are described in WO-A 03/101975, WO-A 2004/037895 and US-A2004/081611.

Particular preference is given to catalytic reactions.

Furthermore, the metal organic framework of the invention can serve assupport, in particular as support for a catalyst.

EXAMPLES Example 1 Preparation of a Pure Al-Fumarate Metal OrganicFramework (MOF)

17.91 g of AlCl₃*6H₂O and 9.04 g of fumaric acid (Linker: Al ratio=1.05mol/mol) are suspended in 550 ml of DMF (solids content=0.05 g/g) in aglass flask and stirred under reflux (130° C.) for 17 hours. The solidformed is filtered off and washed with 3×100 ml of acetone and 2×100 mlof methanol. The filtration time is less than 30 seconds.

The substance is subsequently dried at 100° C. in a vacuum drying ovenfor 16 hours. This gave 11.4 g of a white preproduct. The N₂ surfacearea is measured as 1155 m²/g (Langmuir).

Example 2 Preparation of a Pure Al-Fumarate MOF

17.91 g of AlCl₃*6H₂O and 10.34 g of fumaric acid (Al: Linker ratio=1.2mol/mol) are suspended in 550 ml of DMF (solids content=0.051 g/g) in aglass flask and stirred under reflux (130° C.) for 17 hours. The solidformed is filtered off and washed with 3×100 ml of acetone and 2×100 mlof methanol. The substance is subsequently dried at 100° C. in a vacuumdrying oven for 16 hours. This gave 11.4 g of a white preproduct. The N₂surface area is measured as 1149 m²/g (Langmuir).

Example 3 Preparation of a Pure Al-Fumarate MOF

17.91 g of AlCl₃*6H₂O and 14.64 g of fumaric acid (Al: Linker ratio=1.7mol/mol) are suspended in 550 ml of DMF (solids content=0.058 g/g) in aglass flask and stirred under reflux (130° C.) for 17 hours. The solidformed is filtered off and washed with 3×100 ml of acetone and 2×100 mlof methanol. The substance is subsequently dried at 100° C. in a vacuumdrying oven for 16 hours. This gave 11.4 g of a white preproduct. The N₂surface area is measured as 1271 m²/g (Langmuir).

Example 4 Preparation of a Pure Al-Fumarate MOF

26.9 g of AlCl₃*6H₂O and 15.4 g of fumaric acid (Linker: Al ratio=1.2mol/mol) are suspended in 550 ml of DMF (solids content=0.078 g/g) in aglass flask and stirred under reflux (130° C.) for 96 hours. The solidformed is filtered off and washed with 3×100 ml of acetone and 3×100 mlof methanol. The substance is subsequently dried at 100° C. in a vacuumdrying oven for 16 hours. This gave 18.4 g of a white preproduct. The N₂surface area is measured as 1272 m²/g (Langmuir).

Example 5 Hydrogen Isotherms at 77 K

FIG. 2 shows the H₂ uptake of the MOF according to the invention. Themeasurement is carried out on a commercially available Autosorb-1instrument from Quantachrome. The measurement temperature is 77.4 K. Thesample is pretreated under reduced pressure for 4 hours at roomtemperature and subsequently for a further 4 hours at 200° C. before themeasurement.

FIG. 2 shows the hydrogen capacity K (cc/g at STP) as a function of therelative pressure p/p₀ (p₀=94632.4 torr).

Example 6 Hydrogen Isotherms at 77 K

FIG. 3 shows the H₂ uptake of the Al-fumarate MOF. The measurementtemperature is 77.4 K. The samples are each pretreated under reducedpressure for 4 hours at room temperature and subsequently for a further4 hours at 200° C. before the measurement.

The hydrogen uptake (g/l) is shown as a function of the absolutepressure p (bar).

Example 7 Suitability for CO₂ Separations

Pure substance isotherms are recorded at 42° C. for absorption of CO₂,CO and methane (21° C.) on the material from example 1 (FIG. 4). Thelarge difference between the CO uptake and the CO₂ uptake shows thatthis material in principle has a good selectivity for the separationtasks CO₂/methane and CO₂/CO.

FIG. 4 shows the amount absorbed A (mg/g) as a function of the absolutepressure p (mbar). Here, the curves 1, 2 and 3 correspond to the gasesCO₂, methane and CO.

1-16. (canceled)
 17. A porous metal organic framework comprisingAl^(III) ions and fumarate ions, wherein the Al^(III) ions and thefumarate ions are coordinated in a framework structure.
 18. The porousmetal organic framework according to claim 17, wherein an X-raydiffraction pattern (XRD) of the framework has a basic reflection of8°<2Θ<12°.
 19. The porous metal organic framework according to claim 17,wherein the framework structure has an orthorhombic one-dimensionalchannel structure.
 20. The porous metal organic framework according toclaim 17, wherein the framework is present as a powder and has aspecific surface area of at least 1000 m²/g, determined according to theLangmuir method by N₂ adsorption at 77 K.
 21. A shaped body comprising aporous metal organic framework according to claim
 17. 22. A process forpreparing a porous metal organic framework according to claim 17, theprocess comprising: (i) providing a reaction mixture comprising: atleast one aluminum compound; and fumaric acid or a salt thereof; and(ii) reacting the reaction mixture in the presence of an organic solventat a predetermined temperature and a predetermined pressure.
 23. Theprocess according to claim 22, wherein the aluminum compound comprises ahydrate of an aluminum salt.
 24. The process according to claim 22,wherein the predetermined temperature is 100 to 200° C.
 25. The processaccording to claim 22, wherein the predetermined pressure is 1 to 16 bar(absolute).
 26. The process according to claim 22, wherein reacting thereaction mixture is carried out at a molar ratio of Al^(III) to fumaricacid or its salt of 0.3:1 to 1.7:1.
 27. A method comprising: (i)providing a porous metal organic framework according to claim 17; and(ii) bringing a substance into contact with the porous metal organicframework such that the substance is uptaken by the porous metal organicframework to provide storage of, or controlled release of, thesubstance.
 28. The method according to claim 27, wherein the substancecomprises methane or hydrogen.
 29. A method comprising: (i) providing aporous metal organic framework according to claim 17; and (ii) bringinga substance comprising at least a first component and a second componentinto contact with the porous metal organic framework such that one ofthe first component or the second component is uptaken by the porousmetal organic framework to provide separation of at least one componentfrom the substance.
 30. The method according to claim 29, wherein thesubstance comprises carbon dioxide.
 31. A method comprising: (i)providing a porous metal organic framework according to claim 17; and(ii) bringing a substance into contact with the porous metal organicframework such that the substance is uptaken by the porous metal organicframework and supported thereon.